CN117101264A - Waste water filtering system of cleaning machine - Google Patents
Waste water filtering system of cleaning machine Download PDFInfo
- Publication number
- CN117101264A CN117101264A CN202311325939.0A CN202311325939A CN117101264A CN 117101264 A CN117101264 A CN 117101264A CN 202311325939 A CN202311325939 A CN 202311325939A CN 117101264 A CN117101264 A CN 117101264A
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- China
- Prior art keywords
- enrichment
- porous layer
- shell
- treatment device
- filtration system
- Prior art date
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- 238000001914 filtration Methods 0.000 title claims abstract description 43
- 238000004140 cleaning Methods 0.000 title claims abstract description 25
- 239000002351 wastewater Substances 0.000 title description 18
- 238000000926 separation method Methods 0.000 claims abstract description 23
- 239000002245 particle Substances 0.000 claims abstract description 19
- 239000000706 filtrate Substances 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 16
- 238000004075 wastewater filtration Methods 0.000 claims abstract description 14
- 239000000126 substance Substances 0.000 claims abstract description 11
- 238000004062 sedimentation Methods 0.000 claims abstract description 10
- 238000003825 pressing Methods 0.000 claims abstract description 5
- 239000002910 solid waste Substances 0.000 claims abstract description 5
- 230000003068 static effect Effects 0.000 claims abstract description 5
- 238000003860 storage Methods 0.000 claims description 20
- 239000007921 spray Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 13
- 230000007246 mechanism Effects 0.000 claims description 13
- 238000011010 flushing procedure Methods 0.000 claims description 8
- 239000002893 slag Substances 0.000 claims description 7
- 238000005273 aeration Methods 0.000 claims description 5
- 239000012141 concentrate Substances 0.000 description 15
- 239000007788 liquid Substances 0.000 description 9
- 230000009471 action Effects 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000344 soap Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/56—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/90—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/92—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging filtrate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/94—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging the filter cake, e.g. chutes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/16—Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/30—Filter housing constructions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/04—Non-contaminated water, e.g. for industrial water supply for obtaining ultra-pure water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention relates to the technical field of wastewater filtration, in particular to a wastewater filtration system of a cleaning machine, which comprises: the first treatment device is used for carrying out primary enrichment on the saponified material particles and forming primary enrichment; the separation filter is used for filtering the primary enrichment substance to form a secondary enrichment substance and filtrate; the second treatment device is used for carrying out static sedimentation on the filtrate to obtain tertiary enrichment; and the belt filter press is used for carrying out filter pressing treatment on the secondary enrichment and the tertiary enrichment to obtain solid waste residues. According to the invention, the primary enrichment is filtered through the separation filter to form the secondary enrichment and filtrate, so that the working efficiency is improved and the filtering time is reduced compared with a direct sedimentation mode.
Description
Technical Field
The invention relates to the technical field of wastewater filtration, in particular to a wastewater filtration system of a cleaning machine.
Background
When the cleaning machine is used for cleaning industrial parts, the degreasing cleaning liquid and grease on the surfaces of the industrial parts are subjected to saponification reaction, so that the grease on the surfaces of the industrial parts is removed; in the process, soap substances generated by the reaction are suspended in the wastewater generated in the cleaning process in the form of particles, and if the soap substances are not separated from the wastewater, the repeated utilization of the cleaning wastewater is difficult to realize, so that the waste of water resources is caused; the existing wastewater treatment method is only to enrich and treat soap substance particles in a sedimentation mode after filtration, and the mode is low in efficiency, long in time consumption and incapable of achieving on-line continuous operation.
Disclosure of Invention
The invention aims at overcoming the defects in the prior art and provides a waste water filtering system of a cleaning machine.
The aim of the invention is achieved by the following technical scheme: a washer wastewater filtration system comprising:
the first treatment device is used for carrying out primary enrichment on the saponified material particles and forming primary enrichment;
the separation filter is used for filtering the primary enrichment substance to form a secondary enrichment substance and filtrate;
the second treatment device is used for carrying out static sedimentation on the filtrate to obtain tertiary enrichment;
and the belt filter press is used for carrying out filter pressing treatment on the secondary enrichment and the tertiary enrichment to obtain solid waste residues.
The invention is further arranged that the first processing device comprises a first tank; an aeration pipe is arranged at the bottom of the first storage tank; a first overflow pipe is arranged at the top of the first storage tank; the first overflow pipe is arranged on the separation filter.
The invention is further arranged that the separation filter comprises a housing; the top of the shell is provided with a feed inlet communicated with the first treatment device; the bottom of the shell is provided with a first discharge hole communicated with the second treatment device and a second discharge hole communicated with the belt filter press;
a motor for driving the filter mechanism to rotate is rotationally arranged in the shell; the filtering mechanism comprises a porous layer; a first cavity communicated with the feed inlet is formed in the porous layer; a second cavity is formed between the porous layer and the shell; the first discharging hole and the second discharging hole are respectively communicated with the second cavity.
The invention is further arranged that the filtering mechanism comprises a base and a top cover which are rotatably arranged on the shell; a connecting rod is arranged between the base and the top cover; the porous layer is arranged between the base and the top cover.
The invention is further arranged that a bottom rotating ring is arranged on the base in a rotating way; a top rotating ring is rotatably arranged on the top cover; the porous layer comprises a plurality of first telescopic net wires and a plurality of second telescopic net wires; the first telescopic net wires and the second telescopic net wires are arranged in a staggered mode so that filtering holes are formed;
one end of the first telescopic net wire is arranged on the base; the other end of the first telescopic net wire is arranged on the top rotating ring;
one end of the second telescopic net wire is arranged on the top cover; the other end of the second telescopic net wire is arranged on the bottom rotating ring.
The invention is further arranged that the base and the top cover are both provided with guide grooves; a sliding block is arranged in the guide groove in a sliding manner; a spring abutted against the sliding block is arranged at one end, close to the shell, of the guide groove;
the sliding block penetrates through the guide groove and is provided with a bolt;
the bottom rotating ring and the top rotating ring are respectively provided with a driving groove extending in the involute direction; the bolt is arranged in the driving groove in a sliding mode.
The invention is further arranged that the first cavity is provided with a steam spray pipe and a flushing spray pipe; the steam spray pipes and the flushing spray pipes are provided with spray nozzles facing the porous layer.
The invention is further arranged that a rotating shaft connected with the base is arranged in the first cavity; the rotating shaft is provided with a plurality of rotors;
the shell is provided with a first electromagnetic valve at a first discharge hole; the shell is provided with a second electromagnetic valve at the second discharging hole.
The invention is further arranged that the second treatment device comprises a second tank; a slag discharging pipe is arranged at the bottom of the second storage tank; the slag discharging pipe is communicated with the belt filter press; and a second overflow pipe is arranged at the top of the second storage tank.
The invention has the beneficial effects that: according to the invention, the primary enrichment is filtered through the separation filter to form the secondary enrichment and filtrate, so that the working efficiency is improved and the filtering time is reduced compared with a direct sedimentation mode.
Drawings
The invention will be further described with reference to the accompanying drawings, in which embodiments do not constitute any limitation of the invention, and other drawings can be obtained by one of ordinary skill in the art without inventive effort from the following drawings.
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic view of the first processing apparatus of the present invention;
FIG. 3 is a schematic view of the structure of a second processing apparatus of the present invention;
FIG. 4 is a schematic view of the structure of the separation filter of the present invention;
FIG. 5 is a schematic view of a separator filter according to another aspect of the present invention;
FIG. 6 is a schematic view of the structure of the separation filter of the present invention after concealing the housing;
FIG. 7 is a schematic view of the structure of the separation filter of the present invention after hiding the housing, the first telescoping wire and the second telescoping wire;
FIG. 8 is a schematic view of the structure of the present invention from another view after separating the filter hiding housing, the first telescoping wire and the second telescoping wire;
FIG. 9 is a cross-sectional view of a separation filter of the present invention;
wherein: 1. a first processing device; 11. a first storage tank; 12. an aeration pipe; 13. a first overflow pipe; 2. a second processing device; 21. a second storage tank; 22. a slag discharge pipe; 23. a second overflow pipe; 3. a belt filter press; 4. a separation filter; 41. a housing; 42. a feed inlet; 43. a first discharge port; 44. a second discharge port; 45. a first electromagnetic valve; 46. a second electromagnetic valve; 5. a porous layer; 51. a first cavity; 52. a second cavity; 53. a first telescopic net wire; 54. a second telescopic net wire; 55. a filter hole; 61. a base; 62. a top cover; 63. a connecting rod; 64. a motor; 65. a bottom rotating ring; 66. a top rotating ring; 7. a guide groove; 71. a slide block; 72. a spring; 73. a plug pin; 74. a driving groove; 81. a steam nozzle; 82. flushing the spray pipe; 83. a rotating shaft; 84. a rotor.
Detailed Description
The invention will be further described with reference to the following examples.
As can be seen from fig. 1 to 9, the wastewater filtering system of the cleaning machine according to the present embodiment includes:
a first treatment device 1 for carrying out primary enrichment on saponified material particles and forming primary enrichment;
a separation filter 4 for filtering the primary concentrate to form a secondary concentrate and a filtrate;
the second treatment device 2 is used for carrying out static sedimentation on the filtrate to obtain tertiary enrichment;
and a belt filter press 3 for performing filter pressing treatment on the secondary enrichment and the tertiary enrichment to obtain solid waste residues.
Specifically, the wastewater filtering system of the washing machine in this embodiment includes a first treatment device 1 for performing primary enrichment on saponified particles and forming primary enrichment; the separation filter 4 is used for filtering the primary enrichment to form secondary enrichment and filtrate; the second treatment device 2 is used for carrying out static sedimentation on the filtrate to obtain tertiary concentrate and surface clear liquid; the filter press 3 is used for carrying out filter pressing treatment on the secondary enrichment and the tertiary enrichment to obtain solid waste residues; in this embodiment, the primary concentrate is filtered by the separation filter 4 to form the secondary concentrate and the filtrate, which improves the working efficiency and reduces the filtering time compared with the direct sedimentation mode.
The first treatment device 1 of the wastewater filtering system of the cleaning machine of the embodiment comprises a first storage tank 11; an aerator pipe 12 is arranged at the bottom of the first storage tank 11; a first overflow pipe 13 is arranged at the top of the first storage tank 11; the first overflow pipe 13 is provided to the separation filter 4.
Specifically, when in operation, wastewater generated by the cleaning machine is discharged into the first storage tank 11 of the first treatment device 1, and the surface of micro-bubbles generated by being adsorbed on the aeration pipe 12 under the action of surface tension is brought to the surface of liquid of the first storage tank 11 for enrichment, so as to form a first enriched substance; as the liquid level rises, the first concentrate flows into the separation filter 4 via the first overflow pipe 13.
In the wastewater filtering system of the cleaning machine according to the embodiment, the separation filter 4 includes a housing 41; the top of the shell 41 is provided with a feed port 42 communicated with the first treatment device 1; the bottom of the shell 41 is provided with a first discharge port 43 communicated with the second treatment device 2 and a second discharge port 44 communicated with the belt filter press 3;
a motor 64 for driving the filter mechanism to rotate is rotatably provided in the housing 41; the filtering mechanism comprises a porous layer 5; a first cavity 51 communicating with the feed port 42 is formed in the porous layer 5; a second cavity 52 is formed between the porous layer 5 and the housing 41; the first discharge port 43 and the second discharge port 44 are respectively communicated with the second cavity 52.
Specifically, the first concentrate flows into the first cavity 51 of the filtering mechanism from the feed inlet 42 through the first overflow pipe 13, the motor 64 drives the filtering mechanism to rotate, in the rotating process, saponified material particles with the diameter larger than the pore diameter of the porous layer 5 are trapped inside the porous layer 5 to form a second concentrate, saponified material particles with the diameter smaller than the pore diameter of the porous layer 5 penetrate through the porous layer 5 to enter the second cavity 52 to form filtrate, the filtrate flows into the second processing device 2 through the first discharge hole 43, a settling part in the second processing device 2 forms a third concentrate, and then the third concentrate is conveyed into the belt filter press 3 to be concentrated to form waste residues.
The wastewater filtering system of the cleaning machine of the present embodiment, the filtering mechanism includes a base 61 and a top cover 62 rotatably disposed on the housing 41; a connecting rod 63 is arranged between the base 61 and the top cover 62; the porous layer 5 is provided between the base 61 and the top cover 62. The structure of the filter mechanism is stabilized by the above arrangement, and the base 61 and the top cover 62 can be rotated in synchronization.
In the wastewater filtering system of the cleaning machine according to the embodiment, a bottom rotating ring 65 is rotatably arranged on the base 61; a top rotating ring 66 is rotatably arranged on the top cover 62; the porous layer 5 comprises a plurality of first stretchable mesh wires 53 and a plurality of second stretchable mesh wires 54; the first telescopic net wires 53 and the second telescopic net wires 54 are staggered, so that a filtering hole 55 is formed; one end of the first telescopic net wire 53 is arranged on the base 61; the other end of the first telescopic net wire 53 is arranged on a top rotating ring 66; one end of the second telescopic wire 54 is arranged on the top cover 62; the other end of the second telescopic wire 54 is provided to a bottom rotating ring 65.
Specifically, since the first telescopic wire 53 and the second telescopic wire 54 are fixed at one end to the base 61 or the top cover 62, the other end is fixed to the top rotating ring 66 or the bottom rotating ring 65, and the top rotating ring 66 or the bottom rotating ring 65 is rotatable with respect to the base 61 or the top cover 62; therefore, when the aperture of the filtering holes 55 of the porous layer 5 needs to be changed, only the top rotating ring 66 or the bottom rotating ring 65 needs to be rotated, so that the included angles between the first telescopic net wires 53 and the second telescopic net wires 54 and the horizontal plane are changed, and further the grid interval (i.e. the aperture of the filtering holes 55) formed by the first telescopic net wires 53 and the second telescopic net wires 54 is changed, so as to obtain different interception capacities and improve filtering flexibility.
In the wastewater filtering system of the cleaning machine according to the embodiment, the base 61 and the top cover 62 are provided with guide grooves 7; a sliding block 71 is arranged in the guide groove 7 in a sliding way; a spring 72 abutted against the sliding block 71 is arranged at one end of the guide groove 7 close to the shell 41;
the sliding block 71 penetrates through the guide groove 7 and is provided with a bolt 73;
the bottom rotating ring 65 and the top rotating ring 66 are provided with driving grooves 74 extending in the involute direction; the latch 73 is slidably disposed in the driving slot 74.
Specifically, through the above arrangement, when the aperture of the filtration pore 55 of the porous layer 5 needs to be changed, only the rotation speed of the motor 64 needs to be changed, so that the centrifugal force borne by the sliding block 71 is changed, the sliding block 71 can move against the action of the spring 72, and the first fixing ring and the second fixing ring can be driven to rotate relatively on the base 61 and the top cover 62 through the action of the bolt 73 and the driving groove 74, so that the included angles between the first telescopic net wire 53 and the second telescopic net wire 54 and the horizontal plane are changed, and further the grid spacing (namely the aperture) formed by the first telescopic net wire 53 and the second telescopic net wire 54 is changed, so that different interception capacities are obtained, and the filtration flexibility is improved.
In the wastewater filtering system of the cleaning machine according to the embodiment, the first cavity 51 is provided with a steam nozzle 81 and a flushing nozzle 82; the steam nozzle 81 and the flushing nozzle 82 are each provided with nozzles facing the porous layer 5. In the wastewater filtering system of the cleaning machine according to the embodiment, a rotating shaft 83 connected with the base 61 is disposed in the first cavity 51; the rotating shaft 83 is provided with a plurality of rotors 84; the shell 41 is provided with a first electromagnetic valve 45 at a first discharging hole 43; the housing 41 is provided with a second solenoid valve 46 at the second outlet 44.
Specifically, when in operation, wastewater generated by the cleaning machine is discharged into the first treatment device 1, and is adsorbed under the action of surface tension and the surface of micro-bubbles generated by the aeration pipe 12 is brought to the surface of liquid for enrichment, so as to form a first enrichment; at this time, the second electromagnetic valve 46 is closed, and the first electromagnetic valve 45 is opened; as the liquid level rises, the first concentrate flows into the first cavity 51 of the separation filter 4 through the first overflow pipe 13, and as the filtering mechanism in the separation filter 4 is in a rotating state, the first concentrate entering the first filter impacts the surface of the porous layer 5 under the action of centrifugal force generated by the rotor 84, saponified material particles with the diameter larger than the pore diameter of the filtering holes 55 of the porous layer 5 are trapped inside the porous layer 5 to form second concentrate, and saponified material particles with the diameter smaller than the pore diameter of the filtering holes 55 of the porous layer 5 penetrate through the porous layer 5 to enter the second cavity 52 between the shell 41 and the porous layer 5 to form filtrate; the filtered liquid of the second cavity 52 flows into the second treatment device 2 through the first discharge hole 43, a third enrichment substance is formed at the sedimentation part of the second treatment device 2 and is conveyed into the belt filter press 3 to be concentrated to form waste residues, and supernatant liquid of the second treatment device 2 can flow back to the cleaning machine from the second overflow pipe 23 for reuse;
when the second concentrate is required to be discharged from the first cavity 51 of the separation filter 4, the second electromagnetic valve 46 is opened, the first electromagnetic valve 45 is closed, and the rotating speed of the motor 64 is increased, so that the aperture of the filtering holes 55 of the porous layer 5 is enlarged, and the steam spray pipe 81 sprays high-temperature steam to the porous layer 5 to soften saponified material particles trapped on the surface of the porous layer 5, so that the saponified material particles are more beneficial to reaching the second cavity 52 through the inside of the porous layer 5; as the rotational speed increases, the centrifugal force to which the saponified material particles themselves are subjected increases, making it easier for them to pass through the porous layer 5 into the second cavity 52; after the rotation speed is increased, the sliding block 71 drives the bottom rotating ring 65 and the top rotating ring 66 to further rotate, so that the tension applied to the first telescopic net wire 53 and the second telescopic net wire 54 is increased, the wire diameter of the first telescopic net wire is further contracted, and the diameter of the filtering holes 55 of the porous layer 5 is further enlarged, so that saponified material particles can more easily pass through the inside of the porous layer 5 to the second cavity 52; meanwhile, after the second concentrate is discharged, the flushing spray pipe 82 sprays water to the surface of the porous layer 5 to clean the porous layer 5, at this time, the rotation speed of the motor 64 is reduced, the first telescopic net wire 53 and the second telescopic net wire 54 in a stretched state shrink, the surface area is reduced, so that the saponified material particles remained on the surface of the porous layer are synchronously enriched, and the adhesive force between the saponified material particles and the first telescopic net wire 53 and the second telescopic net wire 54 is synchronously reduced due to the reduction of the effective contact area, so that the cleaning liquid flow is easier to flush the saponified material particles away from the surfaces of the first telescopic net wire 53 and the second telescopic net wire 54, and the cleaning effect is better; at the same time, the saponified material particles attached to the surface of the shell 41 are washed and discharged to the belt filter press 3 through the second discharge port 44 to be further concentrated to obtain waste residues.
The second treatment device 2 of the wastewater filtering system of the cleaning machine of the present embodiment includes a second storage tank 21; the bottom of the second storage tank 21 is provided with a slag discharging pipe 22; the slag discharging pipe 22 is communicated with the belt filter press 3; a second overflow pipe 23 is arranged at the top of the second storage tank 21.
Finally, it should be noted that the above embodiments are only for illustrating the technical solution of the present invention, and not for limiting the scope of the present invention, and although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions can be made to the technical solution of the present invention without departing from the spirit and scope of the technical solution of the present invention.
Claims (9)
1. A cleaning machine waste water filtration system which characterized in that: comprising the following steps:
the first treatment device is used for carrying out primary enrichment on the saponified material particles and forming primary enrichment;
the separation filter is used for filtering the primary enrichment substance to form a secondary enrichment substance and filtrate;
the second treatment device is used for carrying out static sedimentation on the filtrate to obtain tertiary enrichment;
and the belt filter press is used for carrying out filter pressing treatment on the secondary enrichment and the tertiary enrichment to obtain solid waste residues.
2. A washer wastewater filtration system as recited in claim 1 wherein: the first treatment device comprises a first storage tank; an aeration pipe is arranged at the bottom of the first storage tank; a first overflow pipe is arranged at the top of the first storage tank; the first overflow pipe is arranged on the separation filter.
3. A washer wastewater filtration system as recited in claim 1 wherein: the separation filter includes a housing; the top of the shell is provided with a feed inlet communicated with the first treatment device; the bottom of the shell is provided with a first discharge hole communicated with the second treatment device and a second discharge hole communicated with the belt filter press;
a motor for driving the filter mechanism to rotate is rotationally arranged in the shell; the filtering mechanism comprises a porous layer; a first cavity communicated with the feed inlet is formed in the porous layer; a second cavity is formed between the porous layer and the shell; the first discharging hole and the second discharging hole are respectively communicated with the second cavity.
4. A washer wastewater filtration system as recited in claim 3 wherein: the filtering mechanism comprises a base and a top cover which are rotatably arranged on the shell; a connecting rod is arranged between the base and the top cover; the porous layer is arranged between the base and the top cover.
5. The washer wastewater filtration system of claim 4 wherein: a bottom rotating ring is rotatably arranged on the base; a top rotating ring is rotatably arranged on the top cover; the porous layer comprises a plurality of first telescopic net wires and a plurality of second telescopic net wires; the first telescopic net wires and the second telescopic net wires are arranged in a staggered mode so that filtering holes are formed;
one end of the first telescopic net wire is arranged on the base; the other end of the first telescopic net wire is arranged on the top rotating ring;
one end of the second telescopic net wire is arranged on the top cover; the other end of the second telescopic net wire is arranged on the bottom rotating ring.
6. A washer wastewater filtration system as recited in claim 5 wherein: the base and the top cover are both provided with guide grooves; a sliding block is arranged in the guide groove in a sliding manner; a spring abutted against the sliding block is arranged at one end, close to the shell, of the guide groove;
the sliding block penetrates through the guide groove and is provided with a bolt;
the bottom rotating ring and the top rotating ring are respectively provided with a driving groove extending in the involute direction; the bolt is arranged in the driving groove in a sliding mode.
7. The washer wastewater filtration system of claim 4 wherein: the first cavity is provided with a steam spray pipe and a flushing spray pipe; the steam spray pipes and the flushing spray pipes are provided with spray nozzles facing the porous layer.
8. The washer wastewater filtration system of claim 4 wherein: a rotating shaft connected with the base is arranged in the first cavity; the rotating shaft is provided with a plurality of rotors;
the shell is provided with a first electromagnetic valve at a first discharge hole; the shell is provided with a second electromagnetic valve at the second discharging hole.
9. A washer wastewater filtration system as recited in claim 1 wherein: the second treatment device comprises a second storage tank; a slag discharging pipe is arranged at the bottom of the second storage tank; the slag discharging pipe is communicated with the belt filter press; and a second overflow pipe is arranged at the top of the second storage tank.
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